Packaged food products

ABSTRACT

A method for the production of a stabilized packaged food product includes the steps of: filling a tray with a predetermined quantity of a food starting material; introducing the tray into a pressure vessel and conveying the tray through the pressure vessel while performing the following steps in sequence inside the pressure vessel: (i) treating the food starting material with high-temperature pressurized steam to sterilize the material, (ii) dosing the sterile food material inside the tray with a predetermined amount of sterile water; and (iii) applying a lid to the tray to seal the food product inside the tray while maintaining the tray in a sterile environment. Also provided are an apparatus for performing the method and packaged stabilized full moisture food products obtainable by the process.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a national stage filing of PCT/IB2008/002120 filedMay 29, 2008 claiming priority to GB 0710228.8 filed on May 29, 2007; GB0715579.9 filed on Aug. 9, 2007; and GB 0801052.2 filed on Jan. 21,2008.

TECHNICAL FIELD

The present invention relates to stabilized, packaged, full moisturefood products and to methods and apparatus for the preparation thereof.It relates in particular to stabilized, packaged, full-moisture foodproducts containing cereals such as rice, wheat or pasta, and/or otheringredients such as vegetables and meat.

BACKGROUND OF THE INVENTION

It is known to provide packaged, full-moisture precooked food products,such as soups, stews, and rice, pasta or wheat (bulgur) products thatcan be reheated in a short time, for example in a microwave oven. Theseproducts are sometimes referred to as “ready-to-heat” or “one-minute”products.

The high moisture content of these ready-to-heat products requiresspecial steps to be taken in order to render them sufficiently stablefor storage and distribution through conventional retail channels.

U.S. Pat. No. 4,986,995 describes a process for the preparation ofshelf-stable rice. The process includes soaking dry rice in water at 20°C., introducing the rice into a container such as a pouch together withsufficient water to hydrate the rice to a full moisture product, sealingthe pouch with a restricted amount of oxygen in the pouch, and thencooking and sterilizing the rice in the pouch by heating in an autoclaveto a temperature of at least 121° C. The resulting shelf-stable riceproduct can be microwave-heated in the pouch before serving.Unfortunately, the time-temperature-moisture conditions required toachieve sterility cause some chemical modification of the food starch,resulting in a tendency of the full-moisture sterile product toagglomerate over time. As a result of this agglomeration the rice doesnot have the optimum freshly-cooked texture and free-flowing properties.Furthermore, the autoclave cooking within the sealed pouch can result insome undesirable aroma of the product, especially when the pack is firstopened.

EP-A-0602953 describes shelf-stable microwaveable pouches containingfull moisture precooked rice. The rice has been acidified by theaddition of enough edible acid to lower its pH to a range of 3.5 to 4.6.This enables a shelf-stable product to be achieved by heat treatment atlower temperatures than are needed for a non-acidified product,resulting in improved texture and flow properties compared to theautoclaved rice products. Further acid-stabilized rice products aredescribed in U.S. Pat. No. 5,702,745 and EP-A-1338209. Unfortunately,the addition of an edible acid to the rice gives rise to acid flavornotes that reduce consumer acceptability of the product. EP-A-0322996teaches to overcome this problem by packaging the stabilized rice with aneutralising agent that can be mixed with the rice immediately beforeconsumption.

EP-A-0691082 describes a plant for the production of packaged,stabilized, ready-to-heat cooked meals such as pasta. The plantcomprises an autoclave body defining a food-processing chamber having aconveyor therein for conveying open trays containing a food product froman inlet end of the autoclave to an outlet end thereof. The autoclavecomprises, in succession, between the inlet and outlet ends: a) a firstregion which includes means for dispensing steam for the heatstabilisation and/or sterilisation of the food and of the open trays, b)a second region which includes a spray for delivering boiling water forcooking the food in the respective trays, c) a straining region whichincludes a device for inverting the trays for removing the excesscooking liquid from the cooked food while retaining the cooked food inthe respective containers. The system includes a sealing assembly forhermetically sealing the trays. The sealing assembly is located in asterile environment communicating with the sterile cooking chamber.

U.S. Pat. No. 5,860,356 describes a system for providing a sterile,full-moisture packaged rice product. The system includes a rice fillingdevice that fills individual trays with a predetermined quantity ofwashed and soaked rice. The trays are then conveyed through asterilization chamber that substantially air-tightly contains one ormore of arrays of the trays for sterilizing the rice withhigh-temperature pressurized steam introduced into the chamber. Thetrays are then transferred to a steaming chamber separate from thesterilization chamber and at ambient pressure, where a water fillingdevice fills the trays containing the sterilized rice with apredetermined quantity of water necessary for steam rice-cooking, andthe rice is cooked with steam for a suitable period, for example 30minutes. The trays containing the cooked rice are then conveyed to asealing device in a clean booth that applies an air-tight lid to thetrays containing the cooked rice. Since the clean booth does notcompletely prevent contamination of the rice before sealing, thepackaged products are subjected to a final steaming step to achieve thedesired rice quality and stability. Processes of this type are alsodescribed in US-A-20040219267.

The overall processes of EP-A-0691082 and U.S. Pat. No. 5,860,356 arecapital intensive because of the multiple process steps. The totaltime/temperature/moisture exposure of the products is considerable, andin the case of starchy products these processes can result in productsthat are sticky, not free-flowing, and not ideal texture.

BRIEF SUMMARY OF THE INVENTION

In a first aspect, the present invention provides a method for theproduction of a stabilized packaged food product comprising the stepsof: filling a tray with a predetermined quantity of a food startingmaterial; introducing the tray into a pressure vessel and conveying thetray through the pressure vessel while performing the following steps insequence inside the pressure vessel: (i) treating the food startingmaterial with high-temperature pressurized steam to sterilize thematerial, and (ii) dosing the sterile food material inside said traywith a predetermined amount of sterile water; and (iii) applying a lidto the tray to seal the food product inside the tray while maintainingthe tray in a sterile environment.

The feature of steam sterilizing and water dosing the food productsequentially under sterile steam conditions, followed promptly bysealing the trays under sterile conditions in the steam pressure vessel,provides a very rapid route to commercially sterile products withminimum capital assets. It has been found that extended cooking of thefood product following the dosing step is not needed in order to achievea stable, full moisture, ready-to-heat product. Further advantages ofthe process are discussed below.

The initial step of the process comprises filling trays with apredetermined quantity of food starting material. The trays may beformed of any suitable material that is sufficiently heat resistant tokeep its shape in the subsequent steps of the process. Thermoformedpolypropylene (PP), polyethylene terephthalate (PET) or CPET trays maybe suitable, preferably with an ethylene vinyl alcohol (EVOH) oxygenbarrier layer. For example a PP-EVOH-PP laminate may be suitable, withthe PP selected to provide the necessary heat resistance at 135° C. Thelaminate thickness is suitably from about 0.8 mm to about 1.5 mm, forexample about 1 mm to about 1.2 mm. The tray suitably has a bottom,straight or tapered side walls, and a flange (lip) at the top forsealing. The bottom and/or the side walls may be profiled in variousways for decorative or structural reasons. In certain embodiments, thetray may be substantially in the shape of a bowl to assist consumptionof the food product directly from the tray. Metal foil or metal/polymerlaminate trays could also be used, but are not so suitable forsubsequent microwave reheating of the food product before consumption.The tray may include metallised susceptor regions to provide localizedheating in a microwave oven.

The depth of the tray and quantity of starting material are normallyselected so as to produce a substantially filled tray when hydration ofthe contents is complete. The starting material is filled into the traysin a layer (bed) that is preferably not more than about 3 cm deep, forexample from about 0.2 to about 2 cm deep. A uniform bed of food productis desirable, and accordingly the bed height is preferably equalizedbefore performing subsequent steps of the process.

The food starting material in the processes of the present invention maybe any dry or wet solid food material. The process is applicable to bothhuman foods and animal (pet) foodstuffs. The overall moisture content ofthe starting material is suitably less than the overall moisture contentin the packaged product, but in certain embodiments a full moisturestarting material or materials may be used. For example, the foodstarting material may comprise partially or completely dehydrated foodingredients such as freeze-dried meat or vegetable ingredients, ordehydrated milk or sauce components.

The food starting material may alternatively or additionally comprisecooked or uncooked fruit or vegetable pieces, mushroom pieces, nuts,salad pieces, herb pieces, whole herbs such as cloves, anise orcardamom, meat or fish. The starting material pieces may be chilled oreven frozen. Suitably, vegetable starting materials (including potato)are substantially full-moisture. In certain embodiments, the foodstarting material consists of solid soup components, such as meat,vegetable and/or cereal pieces. In these embodiments, a larger amount ofsterile liquid is dosed in the dosing step of the process to result in asterile, liquid soup or sterile soup concentrate containing the solidpieces. It is an advantage of the present process that the relativelybrief heat treatment to which the products are subjected causesrelatively little deterioration of the appearance and texture of freshfood pieces compared to a conventional autoclaving process.

In certain embodiments, the food starting material comprises or consistsessentially of at least one dry starchy component, such as rice, wheat,pulses (e.g. beans or lentils), or pasta pieces. In certain embodiments,at least 10% by weight of the food starting material is made up of suchstarchy components, suitably at least about 50% thereof, for example 90%or more of the food starting material is made up of such starchycomponents. The remainder of the material may be made up of saucecomponents and vegetable, meat or fish components as described.Typically, the non-starchy components are deposited on a bed of thestarchy component in the tray.

The term “dry starchy component” refers to a starchy food startingmaterial having a moisture content below the full moisture content forconsumption of starchy food materials of that type. Suitably, the drystarchy component has a moisture content less than about 30 wt %, forexample less than about 20 wt. %, suitably less than about 16 wt. %. Thedry starchy material typically has a moisture content of about 10-15%,whereby it is storage-stable. The starting material may comprise wholeor comminuted food grains such as rice or wheat grains, couscous,bulgur, or pulses such as beans or lentils. The food grains may be fullymilled (white), or they may have part or all of the bran layer stillattached. The grains may suitably be parboiled. In certain embodiments,the starting material may comprise or consist essentially of dried pastapieces. In other embodiments, the starting material comprises orconsists essentially of dry, milled, parboiled rice having a moisturecontent of about 10% to about 15%. Long-grain rice, basmati rice, Thairice, wild rice and Arborio rice are all suitable for the process of thepresent invention.

It is an advantage of the present invention that the food startingmaterial generally does not require soaking or wetting beforeintroduction into the pressure vessel. Indeed, at least a major portionby weight of the starting material is generally not soaked or wettedbefore introduction into the pressure vessel, since the sterilizationstep is preferably carried out on a dry product in order to minimizeheating time, and to minimize thermal damage to the food components suchas starch. This is a simplification over the process described in U.S.Pat. No. 5,860,356.

The trays containing the food starting material are introduced into apressure vessel, for example through a suitable pressure lock.Preferably the pressure lock permits continuous feeding of the trays tothe pressure vessel. Exemplary pressure locks and tray conveyors aredescribed in EP-A-0691082.

The pressure vessel may consist of a single pressure chamber, or it maycomprise two, three or more pressure chambers separated by pressurelocks. The use of multiple pressure chambers to form the pressure vesselenables process parameters to be controlled further by varying the steampressure and temperature between the chambers. In addition, it allowsindividual pressure chambers to be isolated for cleaning or maintenance.The pressure vessel (or chamber thereof) is suitably in the form of atube having a conveyor therein for conveying the trays along the tube.The diameter of the tube is typically about 30 cm to about 100 cm, forexample about 50 cm. The total length of the pressure vessel (i.e. thesum of the lengths of the pressure chambers) is typically about 10 m toabout 50 m, for example about 15 m to about 40 m. The pressure vessel isthermally insulated to minimise heat loss and steam condensation withinthe vessel. The pressure vessel is pressurized with steam, optionallymixed with other gases. The steam may be saturated or superheated. Thesteam temperature is suitably from about 100° C. to about 160° C.,preferably from about 125° C. to about 150° C., for example about 135°C. The temperature inside the pressure vessel (or each chamber thereof)is thereby maintained substantially at the steam temperature. Suitably,the gauge pressure in the pressure vessel (or each chamber thereof) isfrom about 0.05 MPa to about 1.0 MPa, preferably from about 0.1 MPa toabout 0.5 MPa, for example about 0.3 MPa to about 0.4 MPa. Thetemperatures and pressures in each chamber of the pressure vessel may bethe same or different within the above ranges.

The steam is may be injected through suitable nozzles. In certainembodiments, the steam impinges directly onto the top surface of thefood bed as the trays move through the tube. In other embodiments, thesteam in injected below and/or laterally to the trays. Steam injectionmay be intermittent or continuous. Improved energy efficiency isachieved by using intermittent injection of (preferably saturated)steam, preferably with forced flow inside the pressure vessel tocirculate the steam. The forced flow can be achieved, for example, byproviding fans within the vessel. The high temperature of the steamcauses the core temperature of the food to rise quickly to a valuesufficient to cause rapid sterilization. Uptake of water by the food inthis stage of the process is minimal. Typically, with steam at about135° C., trays containing only rice or wheat are exposed to the steamfor a period of from about 20 seconds to about 1 minute, for exampleabout 20 seconds to about 1 minute. Longer steam sterilization,typically about 3 to about 4 minutes, is needed if the trays containlarger pieces, such as vegetable pieces, meat pieces, or large pastapieces, or if lower steam temperatures are used. The duration of thesteam sterilization step is typically regulated by moving the locationof the water dosing point in the pressure tube, as described furtherbelow. Alternatively or additionally, the duration of the steamsterilization step may be regulated by varying the speed of theconveyor.

The sterilization time and temperature are suitably selected to providea reduction of 12D (i.e. 12 orders of magnitude) of the population ofthe microorganism clostridium botulinum. The minimum lethality factorF_(o) (equivalent to number of minutes of treatment at 121.1° C.) neededto achieve 12D reduction is 2.4 minutes. In practice, a higher lethalityfactor, generally of at least about 3, for example about 5, is appliedin order to provide a safety margin and optionally to inactivate other,more resistant spores, such as B. Stearothermophilus.

It is an advantage of the present invention that the sterilization stepmay be performed on the food while the food is still dry. This avoidsmany of the problems caused by prior art processes in which thesterilization temperatures are applied to hydrated cereal grains, or tocereal grains in contact with liquid water. In particular, the presentinvention results in a more free-flowing final product exhibiting lessdamage to the starch structure, for example exhibiting lessde-retrogradation of the starch and less extrusion of soluble starchesfrom the product grains. Furthermore, the time required to heat the foodparticles to sterilization temperatures is greatly reduced, therebyfurther reducing the process time and damage to the starch and otheringredients as compared to prior art processes.

The food product in the trays is conveyed from the steam sterilizationzone of the pressure vessel to a dosing station (or separate dosingchamber) inside the pressure vessel, where a predetermined amount ofliquid water is dosed into each tray. The pressure and temperatureconditions at the dosing station are suitably within the rangesspecified above for the steam sterilization step, but need not be thesame as those in the steam sterilization step. In particular, the waterdosing may be performed in a chamber that is maintained at a lowoverpressure (e.g. about 0.01-0.3 bar) to maintain sterility. The liquidwater is sterile, and is dosed by means of a suitable pump at atemperature suitably of from about 5° C. to about 150° C., preferablyabout 25° C. to about 99° C.

The term “liquid water” refers to a sterile aqueous liquid. The liquidmay further comprise additives, such as herbs, salt, flavorings,nutrients, acidulents, edible oil and/or edible fat. For example, theliquid may comprise or consist of a stock, a bouillon or a soup base. Itwill be appreciated that the water supply to the dosing nozzles isnormally intermittent, so that water is supplied only to the trays inthe specified amount and no water is wasted. The duration of the waterdosing step is short. Suitably, the liquid water dosing step takes lessthan about 60 seconds, for example less than about 20 seconds, andtypically less than about 10 seconds, for example from about 1 to about5 seconds. There may be more than one water dosing step, optionallyseparated by re-heat steps, especially when a substantial amount ofwater must be dosed, for example in the preparation of soup products.

It is a feature of the present invention that the water is dosed in anamount that is just sufficient to provide a product having the desiredfinal moisture content, i.e. typically about 50 to about 75% moisturefor food grains and pasta. There is substantially no addition or loss ofwater from the product after the dosing step, other than a small amountof condensation from steam in the pressure vessel. This eliminates anyneed to invert the trays in order to drain off excess water. The amountof water dosed is typically from about 0.01 to about 5 g of water pergram of food starting material, for example about 0.01 to 3.5 g/g forrice, and 0.01 to 4 g/g for pasta and couscous. A substantially largeramount of water is dosed for soup products. The measured dosing of waterinside the pressure vessel provides a number of advantages over theprocess of EP-A-0691082, in which the trays are simply sprayed withexcess boiling water. These advantages include reduced energyconsumption, reduced waste water, reduced loss of nutrients, and reducedcapital cost as it is no longer necessary to provide a mechanism todrain the excess water from the product. Likewise, the process of thepresent invention eliminates the need for a separate steaming chamberand prolonged cooking step as described in U.S. Pat. No. 5,860,356. Thepresent inventors have made the surprising finding that simply dosingthe precise amount of water required onto the hot food product, followeddirectly by sealing under sterile conditions, results in an excellent,stable, full-moisture product after a suitable period for moistureequilibration of the product at ambient or moderately elevatedtemperature, as explained further below.

Suitably, directly following the sealing step, the product cooled to atemperature less than about 100° C., is transferred to atmosphericpressure and stored in an environment maintained at less than about 80°C., for example about 25°-80° C., and tempered at this temperature for aperiod of from about 20 minutes to about 4 hours, for example about 30minutes to about 150 minutes, to achieve the desired productcharacteristics. Suitable long-grain rice tempering conditions are 30minutes in an environment maintained at 55° C. followed by 15 minutes inan environment maintained at 45° C. Suitable basmati rice temperingconditions are 30 minutes in an environment maintained at 75° C.,followed by 30 minutes in an environment maintained at 45° C. In certainembodiments, tempering may be achieved by stacking the trays andallowing them to cool to ambient temperature over a period of at leastabout 1 hour, for example 3-4 hours. Certain embodiments, such as soups,do not require any tempering.

Suitably, the temperature of the food bed is at least about 120° C., forexample from about 125° C. to about 150° C. immediately before the wateris dosed. As noted above, it is an advantage of the present inventionthat an extended cooking step is not needed in order to achieve completehydration of the food. Suitably, the interval between the water dosingand sealing of the trays is less about 2 minutes, preferably less thanabout 1 minute, and more preferably less than about 30 seconds Likewise,the interval between the liquid water dosing and removal of the traysfrom the pressure vessel is suitably less than about 2 minutes,preferably less than about 1 minute, and still more preferably less thanabout 30 seconds.

The food product immediately following the dosing and sealing steps maynot be ready to consume, since not all of the water may be absorbedinstantly and the water distribution in the food pieces is not initiallyuniform. Nevertheless, it has been found that the moisture distributionin the food pieces (such as rice grains) becomes uniform within a fewhours at ambient temperature, or after tempering as described above, togive a highly satisfactory product.

The trays containing the hydrated food are sealed by application of alid to the trays while maintaining the trays in the sterile environmentof the pressure vessel (or separate sealing chamber thereof) followingthe dosing step(s) and any optional reheat step(s) following the dosingstep(s). The lid is suitably formed of a film or foil sheet that isstable at the temperature inside the pressure vessel. The cover sheet(lid) may be formed of a suitable heat-resistant laminate comprising asealing layer such as PP and a barrier layer such as EVOH. The thicknessof the cover sheet is suitably from about 50 μm to about 250 μm, forexample from about 100 μm to about 150 μm. The trays are suitablymaintained continuously in a sterile environment between the dosing stepand completion of the sealing step in an atmosphere of steam at atemperature and pressure within the ranges specified above for the steamsterilization and dosing steps. This ensures that sealing is performedunder fully sterile conditions, thereby eliminating the need forsubsequent heat treatment steps to achieve a shelf stable product.

In certain embodiments, the film or foil sheet is fed continuously (as acontinuous strip) into the pressure vessel through a suitable pressurelock. The pressure lock may, for example, comprise a series of rollersor belts between which the sheet is pinched, whereby the pressureapplied across the sheet at any point does not cause permanentcompression of the sheet. The film or foil sheet may be releasablylaminated to a continuous support strip (e.g. a release-coated paper) toprovide the necessary tensile strength after sealing for the residue ofthe film or foil sheet to be wound up. The support strip also enablesthe continuous film or foil sheet to be die-cut with appropriate lidshapes before feeding to the pressure vessel. In other embodiments,pre-cut film or foil lids are fed to the sealing apparatus inside thepressure vessel.

The temperature inside the pressure vessel is sufficient to sterilizethe lid before it is applied. The lid can be attached to the tray inairtight fashion by means of ultrasonic or thermal sealing. Ultrasonicconverters suitable for sealing trays inside sterile enclosures aredescribed, for example, in WO96/09932.

In any event, the hydrated food product inside the trays preferablyexits from the pressure vessel at a temperature sufficiently low toavoid the risk that steam pressure inside the sealed package could causethe package to burst. For example, the food product may return toambient pressure at a temperature less than about 110° C., suitablyabout 100° C. or less. For this purpose, the outlet pressure lock maycomprise a cooling stage.

An important advantage of the processes according to the presentinvention is the short processing time. The total residence time of thetrays in the pressure vessel is typically from about 20 seconds to about6 minutes, for example from about 30 seconds to about 4 minutes. Thetotal treatment time of the trays from entry into the pressure vessel toexit of the sealed trays from the pressure vessel (or the sealingchamber, when sealing is performed in a separate chamber) to the ambientatmosphere is typically from about 20 seconds to about 6 minutes, forexample from about 30 seconds to about 5 minutes. The total treatmenttime depends primarily on the recipe. The processing time for plain riceproducts is at the low end of the above ranges. The processing time formore complex recipes containing vegetable pieces is at the long end ofthe above ranges.

For example, a typical protocol for the preparation of a sterilefull-moisture rice product from parboiled long-grain rice comprisessteam sterilization for 24 seconds (excluding a few seconds for in-feedand out-feed time), followed by dosing (about 2 seconds). In some cases,e.g. for basmati rice, the dosed rice is held for a further 30 secondsin the pressure vessel to heat up the mixture of liquid and solids priorto sealing.

No pre-processing of the food by soaking or wetting is required for mostingredients (pulses and mushrooms may benefit from a preliminary soak).No post-processing of the packaged product by steaming or cooking atenvironmental temperatures above about 80° C. is normally required. Aswell as giving a less thermally degraded product, the present high-speedprocess requires less capital for equipment than most previousprocesses, and less energy. It can be seen that a further advantage ofthe process according to the present invention is that it generates onlyminimal quantities of waste water. A further advantage of the presentprocess is that it is a robust aseptic process that normally does notrequire the use of a clean room or booth.

Accordingly, in a further aspect, the present invention provides amethod for the production of a stabilized packaged food productcomprising the steps of: filling a tray with a predetermined quantity ofa food starting material, followed by performing the following steps insequence while maintaining the tray in a sterile environment: (a)treating the food starting material with high-temperature pressurizedsteam in a pressure vessel to sterilize the material; (b) dosing thesterile food material inside said tray with a predetermined amount ofsterile water; and (c) applying a lid to the tray to seal the foodproduct inside the tray; followed by removing the tray from the sterileenvironment, wherein the residence time of the tray in the sterileenvironment is less than about 10 minutes. Suitably, the residence timeis less than about 6 minutes, for example from about 20 seconds to about6 minutes, typically from about 30 seconds to about 5 minutes.

In a further aspect, the present invention provides a method for theproduction of a stabilized packaged food product comprising the stepsof: filling a tray with a predetermined quantity of a food startingmaterial, followed by performing the following steps in sequence whilemaintaining the tray in a sterile environment: (a) treating the foodstarting material with high-temperature pressurized steam in a pressurevessel to sterilize the material; (b) dosing the sterile food materialinside said tray with a predetermined amount of sterile water; and (c)applying a lid to the tray to seal the food product inside the tray;followed by removing the tray from the sterile environment, wherein theduration of the process from the start of step (a) to the completion ofstep (c) is less than about 10 minutes. Suitably, said duration is lessthan about 6 minutes, for example from about 20 seconds to about 6minutes, typically from about 30 seconds to about 5 minutes.

In a further aspect, the present invention provides a method for theproduction of a stabilized packaged food product comprising the stepsof: filling a tray with a predetermined quantity of a food startingmaterial, followed by performing the following steps in sequence whilemaintaining the tray in a sterile environment: (a) treating the foodstarting material with high-temperature pressurized steam in a pressurevessel to sterilize the material; (b) dosing the sterile food materialinside said tray with a predetermined amount of sterile water; and (c)applying a lid to the tray to seal the food product inside the tray;followed by removing the tray from the sterile environment, wherein thefood material is not subjected to a cooking step subsequent to step (b).

The term “cooking step” in the above aspect refers to a heat treatmentof the product by exposure of the product to an environmentaltemperature above about 80° C. for a period greater than about 10minutes. Suitably, the product according to this aspect is transferredto an environment held at a temperature less than about 80° C., forexample less than about 60° C., within about 10 minutes, preferablywithin about 5 minutes of the completion of the water dosing step (b).

In a further aspect, the present invention provides a method for theproduction of a stabilized packaged food product comprising the stepsof: filling a tray with a predetermined quantity of a food startingmaterial, followed by performing the following steps in sequence whilemaintaining the tray in a sterile environment: (a) treating the foodstarting material with high-temperature pressurized steam in a pressurevessel to sterilize the material; (b) dosing the sterile food materialinside said tray with a predetermined amount of sterile water; and (c)applying a lid to the tray to seal the food product inside the tray;followed by removing the tray from the sterile environment, wherein amajor portion by weight of the food material is not subjected to awetting or soaking step prior to step (a). The term “a major portion”refers to at least about 50%, for example at least about 75%.

All of the various features described above in relation to the firstaspect of the present invention are likewise applicable to the methodsaccording to the further aspects of the invention.

In methods according to the further aspects of the invention, sealingmay be performed either in the pressure vessel, or the trays may betransferred from the pressure vessel to a separate sealing chamber orclean booth in sterile communication with the pressure vessel for thesealing step, for example as described in EP-A-0691082. The film or foilsheet may be fed to the sealing chamber or clean booth, with suitablesterilizing means (e.g. steam, UV or peroxide) provided as appropriate.The sealing chamber or clean booth may suitably be maintained atsubstantially ambient pressure or a slight overpressure (e.g. about 0.01bar to about 0.3 bar) with sterile filtered air or steam.

In a further aspect, the present invention provides an apparatus for theproduction of a stabilized packaged food product comprising: a fillingdevice for filling individual trays with a predetermined amount of afood starting material; a pressure vessel having an inlet pressure lockand an outlet pressure lock for transferring said trays into and out ofthe pressure vessel; a supply of pressurized steam for sterilizing thefood starting material in said trays in a first zone of the pressurevessel; a supply of sterile water and a dosing pump for dosing apredetermined amount of sterile water into each of said trays in asecond zone of the pressure vessel; and a sealing device located in saidpressure vessel for sealing the trays following said step of dosing.

Suitably, the apparatus according to this aspect of the inventioncomprises a conveyor for conveying the trays through the pressurevessel. The pressure vessel may comprise two or more pressure chambers,as described above. Suitably, the apparatus according to this aspect ofthe invention is adapted for operation of a process according to thefirst aspect of the invention. All optional features described above inrelation to the first aspect are likewise applicable to the apparatusaccording to the present aspect.

The term “dosing pump” refers to any pressurizing and dosing apparatusfor supplying predetermined doses of liquid to the trays inside thepressure vessel. The dosing pump is suitably adapted for intermittentoperation, whereby the pump is operated intermittently to dose waterinto the trays in the pressure vessel. The apparatus may comprise aplurality of dosing pumps for sequentially dosing each product more thanonce.

Suitably, the outlet of the pressure vessel or of the separate sterilesealing chamber, communicates in airtight fashion directly with theambient atmosphere or with a tempering chamber for tempering the productat an environmental temperature below about 80° C. That is to say, thesaid outlet does not communicate with a further cooking or steamingchamber.

A further advantage of the processes of the present invention is thatthe resulting stable, packaged ready-to-heat food products do notexhibit the undesirable aroma that can be experienced with in-pouchsterilized precooked products. This advantage could be due to the factthat the present process performs the high-temperature and short-timesterilization on open trays of the products, whereby undesirable aromasevaporate from the product before sealing. Alternatively oradditionally, the low moisture content of the product during thehigh-temperature and short-time sterilization step will reduce thedevelopment of the undesirable aroma compounds. In particular, gaschromatography of rice products made according to the invention showlower levels of odorous aldehydes, in particular heptanal and2,4-decadienals, than were found in pouched ready-to-heat rice products.

Accordingly, in a further aspect, the present invention provides astabilized, packaged, full-moisture food product obtainable by a processaccording to the invention.

The term “stabilized” signifies that the product exhibits reducedspoilage upon storage under ambient conditions as compared to a productthat has been cooked and packaged under ambient air. Suitably, the foodproducts are shelf-stable or ambient-stable. The term “shelf stable”refers to a product that can be stored at typical chill cabinettemperatures of about 7° C. for a period of at least 1 month, preferablyat least 3 months, more preferably at least 6 months and most preferably1 year, without unacceptable deterioration of organoleptic properties orappearance, or without developing microbiological activity outsideregulatory limits. By “ambient stable” is meant a product that canlikewise be stored at typical ambient temperatures, such as 20-25° C. at60% relative humidity, with similar stability.

In certain embodiments, the food products are commercially sterile.Commercial sterility is defined as freedom from viable forms ofmicro-organisms having public health significance, as well as anymicro-organisms of non-health significance capable of reproducing in thefood under the normal non-refrigerated conditions of storage anddistribution. In yet other embodiments, the food products may besterile, that is to say completely free from viable microorganisms.

The term “full-moisture” implies that the moisture content of the foodproduct is sufficient to produce a normal, edible product withoutfurther hydration. For food products such as rice, wheat or pasta thefull moisture content is in the range of from about 50 wt. % to about 75wt. % moisture. The full moisture products may therefore beready-to-heat products. In other embodiments, such as salads, theproducts may be ready to consume directly at ambient temperature,without reheating. In yet other embodiments, such as soup concentrates,the products are fully hydrated but may be suitable for dilution byaddition of water to produce a more palatable product.

The food product obtainable by the invention may optionally beacidified, for example salad products (e.g. pasta salad, rice salad) maybe acidified to achieve the desired flavor. However, the products areusually sufficiently sterile to be ambient shelf-stable without any needfor added acid. Suitably, the pH of the packaged stabilized food productis greater than about 5, for example greater than about 5.5. The pH isdetermined by liquidising the food product with an equal weight ofdistilled water in a blender to form a slurry, and measuring the pH ofthe slurry with a conventional pH electrode.

The packaging is normally in the form of a tray having a bottom, sidewalls, a flange (lip) extending around the top of the side walls, and aflexible sheet lid bonded to the flange to form amicroorganism-impermeable closure. The packaging is substantiallyimpermeable to microorganisms, and it is also substantially impermeableto gases such as oxygen, in order to maintain the freshness of theproduct. Preferably, the packaging is substantially oxygen-impermeable.Suitable packaging materials have an oxygen permeability at 23° C./50%relative humidity less than about 2 cm³/m²/day at 1 atm pressure.Suitably, the lid has been bonded to the flange by ultrasonic bonding.Suitably, the packaging is substantially free of metallic material sothat it can be reheated in a microwave oven. In certain embodiments,metallised susceptor regions may be provided to enhance microwaveheating. Suitably, all components of the packaging have a softeningtemperature greater than about 120° C., preferably greater than about125° C., for example greater than about 140° C.

The components of the food product and packaging are suitably asdescribed above in relation to the first aspect of the invention.Accordingly, the packaged product preferably comprises or consistsessentially of full moisture starchy pieces, such as rice grains.

BRIEF DESCRIPTION OF THE DRAWINGS

An embodiment of the present invention will now be described further,with reference to the accompanying drawing, in which:

FIG. 1 shows a schematic sectional view of an apparatus according to theinvention;

FIG. 2 shows a detail of the dosing and sealing regions of the apparatusof FIG. 1; and

FIG. 3 shows a perspective view of a packaged food product according tothe invention.

DETAILED DESCRIPTION OF THE INVENTION

Referring to FIG. 1, the apparatus comprises a tray filling zone 1, aninlet pressure lock 2, a pressure vessel 3, and an outlet pressure lock4.

The tray filling zone 1 comprises filling stations for loading the trays5 before they are introduced into the pressure vessel 3. The fillingstations comprise a rice filling station 21 and a non-rice fillingstation 22 for depositing non-rice food pieces such as carrot ormushroom on top of the rice bed. Each filling station comprises a hopper23, a feeding device 24 and a dosing device 25. Trays 5 are fed from twostacks 26 to two conveyors 27,28 for filling and supply to the inletpressure lock 2. It will be appreciated that the apparatus may comprisefurther filling lanes, for example 6, 8 or 12 filling lanes, in order toachieved the desired filling rate of the trays.

The pressure vessel 3 is in the form of a tube of length up to 50 m anddiameter approximately 50 cm. The tube is thermally insulated tominimize heat losses. The tube may be subdivided into two or morechambers by pressure locks (not shown) to assist with maintenance and toprovide better control of process conditions.

A conveyor 10 is provided within the tube to move trays 5 containing thefood product from the inlet to the outlet thereof. The pressure vesselcomprises a sterilization zone 7, a water dosing zone 8, and a sealingzone 9. The sterilization zone 7 of the tube 1 proximate to the inletend is provided with steam spray nozzles 6 for spraying hot steam ontothe product bed in trays 5. The steam is supplied from a suitable steamgenerator 11 through a manifold to the nozzles 6. The temperature of thesteam is about 135° C., and the pressure is about 0.3 MPa gauge. Fans(not shown) may be provided to circulate the steam inside the pressurevessel. It has been found that a sterilization time of about 24-30 s issufficient for dry parboiled long-grain rice, and a sterilization timeof about 120 s or more is necessary for 1 cm³ pieces of fresh vegetablessuch as carrot.

The conveyor 10 extends from the sterilizing zone 7 of the pressure tubeto the water dosing zone 8. Referring to FIG. 2, the water dosing zoneof the apparatus comprises a water supply 13, pump 14 and watersterilizer 15 for dosing predetermined amounts of sterilized aqueousliquid from a nozzle into the trays containing sterile dry rice in thedosing zone. It will be appreciated that more than one dosing apparatusmay be provided in the dosing zone to sequentially dose largerquantities of liquid, for example when making soups, with re-heat zonesbetween the dosing apparatuses. The water supplied may containadditional ingredients such as salt, oil, herbs, spices, vegetableparticles, bouillon or flavorings. The location of the dosing zone 8 maybe moved, depending on the time required for the sterilization step.That is to say, the dosing zone is moved further down the tube if alonger sterilization step is required assuming constant conveyor speed.Alternatively or additionally, the conveyor speed may be adjusted tovary the duration of the steam sterilization step. Just sufficient wateris added in the dosing step to increase the moisture content of the riceto about 65-67 wt. %. The temperature of the liquid is adjusted withinthe range about 5° C. to about 140° C., for example from about 25° C. toabout 100° C. depending on the parameters of the system. The waterdosing zone 8 is shorter than the sterilizing zone 7, since the timetaken to dose the water is very short. The conveyor then extends to asealing zone 9. The apparatus further comprises an ultrasonic or thermalsealing tool 17 for sealing a plastics foil lid to the trays in thesealing zone. The trays in the sealing zone are lifted into contact withthe ultrasonic sealing tool by movable anvil 18. The foil lid is cutfrom a continuous web 19 of the plastics foil that is fed through asuitable pressure port 20 in the pressure tube. In alternativeembodiments, the sealing is performed in a separate sealing chamber insterile communication with the pressure vessel 3, i.e. downstream of,and in sterile communication with, the pressure lock 3.

The apparatus does not comprise any steaming or cooking equipmentdownstream of the outlet port. It is an advantage of the apparatus andmethod of the present invention that no cooking of the packaged productsat environmental temperatures above about 80° C. is needed. It is merelynecessary to store the products at an environmental temperaturetypically in the range 40° C.-80° C. for a few hours to achieve astable, packaged, ready-to-heat rice and vegetable product.

Referring to FIG. 3, the packaged food product 30 according to theinvention comprises full-moisture shelf-stable long-grain rice packagedin a thermoformed tray 32 having a flanged top 34, to which ishermetically bonded a film lid 36.

Reference Example 1

A bench-top simulation of the method according to the invention wasperformed as follows. A polypropylene tray was filled to a depth ofabout 1cm with dry, milled, parboiled long-grain rice having moisturecontent about 14 wt. %. The tray was introduced into a modified smallretort and treated with steam at 135° C. for a time sufficient toachieve F_(o) of 5 minutes. The tray was then removed from the retortand liquid water at 100° C. was immediately added in an amount justsufficient to bring the total water content of the rice up to 65 wt. %.The tray was then immediately sealed by ultrasonically bonding apolypropylene film over the top of the tray. The tray and contents werethen left to equilibrate for 30 minutes to 150 minutes at temperaturesin the range 40° C. to 80° C.

The packaged rice product obtained by this method was ambient stable andhad a natural, freshly cooked appearance. It could be reheated forimmediate consumption. The reheated product was completely free-flowing.None of the undesirable aroma of prior art ready-to-heat pouched ricewas detected. Analysis of the rice aroma by gas chromatography—massspectrometry (GCMS) showed reduced levels of certain aroma aldehydesrelative to conventional, ready-to-heat pouched rice. In particular,levels of heptanal and 2,4-decadienals were reduced. These aldehydes areproduced primarily by fat oxidation. The analysis also revealed theabsence of certain hydrocarbon (alkane) components that are present inthe conventional pouched ready-to-heat rice products. It is thought thatthese alkane components may be derived from the packaging material underthe conventional high-temperature sterilization conditions.

The above embodiment has been described by way of example only. Manyother embodiments falling within the scope of the accompanying claimswill be apparent to the skilled reader.

1. A method for the production of a stabilized packaged food productcomprising the steps of: filling a tray with a predetermined quantity ofa food starting material; introducing the tray into a pressure vesseland conveying the tray through the pressure vessel while performing thefollowing steps in sequence inside the pressure vessel: (i) treating thefood starting material with high-temperature pressurized steam tosterilize the material, (ii) dosing the sterile food material insidesaid tray with a predetermined amount of sterile water; and (iii)applying a lid to the tray to seal the food product inside the traywhile maintaining the tray in a sterile environment.
 2. The methodaccording to claim 1, wherein the food starting material comprises oneor more starchy food pieces having a moisture content of less than about30 wt. %.
 3. The method according to claim 1, wherein the food startingmaterial is selected from the group consisting of cooked fruit orvegetable pieces, uncooked fruit or vegetable pieces, nuts, spices,mushroom pieces, salad pieces, herb pieces, meat and fish.
 4. The methodaccording to claim 1, wherein the food starting material is sterilizedby treatment with steam in said pressure vessel at a temperature of fromabout 125° C. to about 150° C.
 5. The method according to claim 1,wherein the step of dosing the sterile food material with sterile wateris initiated while the temperature of the food material is from about125° C. to about 150° C.
 6. The method according to claim 1, wherein thestep of applying the lid to the tray to seal the food product inside thetray is performed in a pressurized sealing chamber in sterilecommunication with the rest of the pressure vessel.
 7. The methodaccording to claim 1, wherein the step of applying the lid to the trayto seal the food product inside the tray is performed not more thanabout 3 minutes after said step of dosing.
 8. The method according toclaim 1, wherein the total residence time of each said tray inside thepressure vessel is from about 30 seconds to about 5 minutes.
 9. Themethod according to claim 1, further including the step of removing thepackaged food product from the pressure vessel wherein nopost-processing of the packaged food product is required.
 10. The methodaccording to claim 1, wherein at least a major portion by weight of thefood starting material is not subjected to a soaking or wetting stepprior to introduction of the material into the pressure vessel.
 11. Anapparatus for the production of a stabilized packaged food productcomprising: a filling device for filling individual trays with apredetermined amount of a food starting material; a pressure vesselhaving an inlet pressure lock and an outlet pressure lock fortransferring said trays into and out of the pressure vessel; a means ofsupplying pressurized steam for sterilizing the food starting materialin said trays in a first zone of the pressure vessel; a means ofsupplying sterile water and a dosing pump for dosing a predeterminedamount of sterile water into each of said trays in a second zone of thepressure vessel to achieve a desired full moisture food product in thetrays; and a sealing device located in said pressure vessel for sealingthe trays following said step of dosing.
 12. The apparatus according toclaim 11, wherein the pressure vessel is divided into two or morechambers, separated by pressure locks.
 13. (canceled)
 14. A method forthe production of a stabilized packaged food product comprising thesteps of: filling a tray with a predetermined quantity of a foodstarting material, followed by performing the following steps insequence while maintaining the tray in a sterile environment: (a)treating the food starting material with high-temperature pressurizedsteam in a pressure vessel to sterilize the material; (b) dosing thesterile food material inside said tray with a predetermined amount ofsterile water; and (c) applying a lid to the tray to seal the foodproduct inside the tray; removing the tray from the sterile environment,wherein the duration of the process from the start of step (a) to thecompletion of step (c) is less than about 10 minutes.
 15. A method forthe production of a stabilized packaged food product comprising thesteps of: filling a tray with a predetermined quantity of a foodstarting material, followed by performing the following steps insequence while maintaining the tray in a sterile environment: (a)treating the food starting material with high-temperature pressurizedsteam in a pressure vessel to sterilize the material; (b) dosing thesterile food material inside said tray with a predetermined amount ofsterile water; and (c) applying a lid to the tray to seal the foodproduct inside the tray; removing the tray from the sterile environment,wherein the food material is not subjected to a cooking step subsequentto step (b).
 16. A method for the production of a stabilized packagedfood product comprising the steps of: filling a tray with apredetermined quantity of a food starting material, followed byperforming the following steps in sequence while maintaining the tray ina sterile environment: (a) treating the food starting material withhigh-temperature pressurized steam in a pressure vessel to sterilize thematerial; (b) dosing the sterile food material inside said tray with apredetermined amount of sterile water; and (c) applying a lid to thetray to seal the food product inside the tray; removing the tray fromthe sterile environment, wherein at least a major portion by weight ofthe food material is not subjected to a wetting or soaking step prior tostep (a).
 17. The method of claim 7, wherein the step of applying thelid to the tray to seal the food product inside the tray is performednot more than about 2 minutes after said step of dosing,
 18. The methodof claim 17, wherein the step of applying the lid to the tray to sealthe food product inside the tray is performed not more than about 1minute after said step of dosing.